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CN106083675A - A kind of methionine novel crystal forms I and preparation method thereof - Google Patents

A kind of methionine novel crystal forms I and preparation method thereof Download PDF

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Publication number
CN106083675A
CN106083675A CN201610391281.7A CN201610391281A CN106083675A CN 106083675 A CN106083675 A CN 106083675A CN 201610391281 A CN201610391281 A CN 201610391281A CN 106083675 A CN106083675 A CN 106083675A
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methionine
crystal formation
solution
diffraction
preparation
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CN201610391281.7A
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CN106083675B (en
Inventor
吴传隆
万霞
刘丹
刘桢
李华萍
金海琴
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Ningxia Ziguang Tianhua Methionine Co Ltd
Ningxia Unisplendour Tianhua Methionine Co Ltd
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Ningxia Ziguang Tianhua Methionine Co Ltd
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Priority to PCT/CN2017/084383 priority patent/WO2017206703A1/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C319/00Preparation of thiols, sulfides, hydropolysulfides or polysulfides
    • C07C319/26Separation; Purification; Stabilisation; Use of additives
    • C07C319/28Separation; Purification
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C323/00Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups
    • C07C323/50Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and carboxyl groups bound to the same carbon skeleton
    • C07C323/51Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and carboxyl groups bound to the same carbon skeleton having the sulfur atoms of the thio groups bound to acyclic carbon atoms of the carbon skeleton
    • C07C323/57Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and carboxyl groups bound to the same carbon skeleton having the sulfur atoms of the thio groups bound to acyclic carbon atoms of the carbon skeleton the carbon skeleton being further substituted by nitrogen atoms, not being part of nitro or nitroso groups
    • C07C323/58Thiols, sulfides, hydropolysulfides or polysulfides substituted by halogen, oxygen or nitrogen atoms, or by sulfur atoms not being part of thio groups containing thio groups and carboxyl groups bound to the same carbon skeleton having the sulfur atoms of the thio groups bound to acyclic carbon atoms of the carbon skeleton the carbon skeleton being further substituted by nitrogen atoms, not being part of nitro or nitroso groups with amino groups bound to the carbon skeleton
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B2200/00Indexing scheme relating to specific properties of organic compounds
    • C07B2200/13Crystalline forms, e.g. polymorphs

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A kind of methionine crystal formation I, described crystal formation I angle of diffraction 2 θ 21.751 ± 0.2 °, 22.168 ± 0.2 °, 21.186 ± 0.2 °, 25.426 ± 0.2 °, 18.395 ± 0.2 °, have diffraction maximum at 32.879 ± 0.2 °.Methionine crystal formation I of the present invention is that white crystals granule, reflective are good; its granule is big, in near-spherical and granularity concentrates on 110 130 microns, more uniform, excellent quality; its dissolubility is good simultaneously; in water, dissolubility is more than 4.5g/100g water, uses it for efficiency height during liquid preparation produces, is beneficial to large-scale industrial use production.

Description

A kind of methionine novel crystal forms I and preparation method thereof
Technical field
The present invention relates to a kind of methionine novel crystal forms and preparation method thereof.
Background technology
Methionine (DL-Methionine) chemical formula is C5H11O2NS, white flakes crystallization or crystalline powder, there is spy Different abnormal smells from the patient, taste is micro-sweet.For nutritional supplement, add in Herba bromi japonici, rye (Secale cereale L.), rice, Semen Maydis, Semen Tritici aestivi, peanut powder, Semen sojae atricolor, Rhizoma Solani tuber osi, Herba Spinaciae Deng in food to improve amino acid balance, requirement is different with cystine intake, adult man's requirement be 1.1g/d.Also use In amino acid transfusion, comprehensive amino acid preparation, can be used as spice by China GB2760-86 regulation, it or one are essential Animal feed additive, the animal feed added with methionine can help animal Fast Growth at short notice so that it is save The feedstuff of about 40%.Poultry lack methionine, can cause dysplasia, lose weight, Liver and kidney miopragia, amyotrophy, Fur is rotten.
Chinese patent CN104926701 A discloses the purifying process of a kind of methionine, uses macroporous adsorbent resin to separate Methionine and by-product salts substances, methionine is attracted on macroporous adsorbent resin then reclaim egg ammonia with strippant desorbing resin Acid, by-product salts substances is not entered in absorption effluent by absorption with macroporous adsorbent resin in adsorption process, mainly includes following Step: 1) resin absorption: methionine solution passes through macroporous adsorbent resin layer, when containing methionine in resin column effluent When content is more than or equal to 10% (w/w) of import content, stop resin absorption;Resin absorption effluent is as by-product salt thing Matter;2) resin desorption: step 1) in complete the resin of absorption, pass through with strippant, desorbing resin, and collect solution Imbibition;3) subsequent technique process: stripping liquid is according to existing technological process subsequent treatment.Through Adsorption and desorption technique, available pure The methionine product of degree >=99%, methionine content≤0.03% in by-product salts substances, resin extraction methionine yield >= 98%.Chinese patent CN104177280 A discloses a kind of methionine production technology, step 1: passed through by methionine crystalline mother solution The continuous chromatography piece-rate system being filled with sodium form or potassium type chromatography resin separates, and obtains methionine solution and inorganic salt solution;Step Rapid 2: methionine solution uses counter-infiltration system be concentrated to give methionine reverse osmosis concentrated liquid, by reverse osmosis concentrated for the methionine obtained Contracting liquid returns Crystallization Procedure;This technique is simple, good separating effect, the advantages such as methionine purity is high, concentrated cost is low.
China granted patent CN101480385 B discloses the purposes of a kind of methionine, and methionine is in preparation treatment or pre- Purposes in the compositions of anti-vestibulum auris internae hair cell disease, contains in its pharmaceutical composition: (a) 50-200 weight portion methionine And/or its polypeptide;The pharmaceutically acceptable carrier of (b) 400-2000 weight portion;And the weight of (a)+(b) is that pharmaceutical composition is total The 50-99% of weight, described pharmaceutical composition is solid preparation or liquid preparation, described liquid preparation include opacifiers, Solution, suspending agent, syrup, drop etc..
The granules of methionine product solubility produced at present is relatively low, at about 3g/100g, use it in liquid preparation raw Produce inefficient, there is certain limitation.
Summary of the invention
It is an object of the invention to provide the methionine novel crystal forms I that a kind of dissolubility is good.
Another object of the present invention is to provide the preparation method of above-mentioned methionine novel crystal forms I.
The object of the invention is achieved through the following technical solutions:
A kind of methionine crystal formation I, it is characterised in that: described crystal formation angle of diffraction 2 θ 21.751 ± 0.2 °, 22.168 ± 0.2 °, 21.186 ± 0.2 °, 25.426 ± 0.2 °, 18.395 ± 0.2 °, have diffraction maximum at 32.879 ± 0.2 °.This crystal formation produces Product dissolubility is excellent.
Specifically, methionine crystal formation I of the present invention angle of diffraction 2 θ 18.395 ± 0.2 °, 21.186 ± 0.2 °, 21.751±0.2°、22.168±0.2°、23.301±0.2°、25.426±0.2°、32.879±0.2°、33.775± 0.2 °, 37.054 ± 0.2 °, have diffraction maximum at 42.455 ± 0.2 °.
Above-mentioned methionine crystal formation I, it is characterised in that: it has followingValue and relative intensity percentage ratio I (%) value Express-X-ray powder diffraction data,
Specifically, above-mentioned methionine crystal formation I, it is characterised in that: it has followingValue and relative intensity percentage Express than I (%) value-X-ray powder diffraction data,
More specifically, above-mentioned methionine crystal formation I, it is characterised in that: it has X-ray powder diffraction as shown in Figure 1 Figure.
The melting point peak temperature of above-mentioned methionine crystal formation I is 282 DEG C, and this crystal formation has DSC/TG collection of illustrative plates as shown in Figure 2.
Methionine crystal formation I of the present invention is identical with methionine chemical constitution, and quality better, to be used for producing liquid preparation raw Product efficiency is high.
The preparation method of methionine crystal formation I of the present invention, employing following steps:
1,5-(β-first mercaptoethyl) hydantoin react with solution of potassium carbonate obtain containing methionine potassium hydrolyzed solution The hydroxypropyl methyl cellulose of middle addition 50-1000ppm, is passed through CO while stirring2、CO2The pressure that is passed through be 0.2-0.6Mpa, Carry out crystallization and obtain methionine crude product;
2, above-mentioned methionine crude product is dissolved in sec-butyl alcohol solvent with the concentration of 10mg/mL-50mg/mL, is stirred continuously, It is heated to 60 DEG C~100 DEG C dissolvings, filters, form supersaturated solution;The sealing of this solution is placed in-5 DEG C~-10 DEG C of environment Crystallisation by cooling 1-3 hour, obtains white crystal.
The present invention has a following beneficial effect:
Methionine crystal formation I of the present invention is that white crystals granule, reflective are good, and its granule is big, in near-spherical and granularity is concentrated In 110-130 micron, more uniform, excellent quality, its dissolubility is good simultaneously, and in water, dissolubility is more than 4.5g/100g water, will Efficiency in liquid preparation produces is high for it, be beneficial to large-scale industrial use produces.
Accompanying drawing explanation
Fig. 1 is crystal type methionine X-ray powder diffraction figure of the present invention;
Fig. 2 is differential scanning calorimeter (DSC)/thermogravimetric analysis (TG) figure of crystal type methionine of the present invention;
Fig. 3 is the crystal type methionine of the present invention scanning electron microscope (SEM) photograph under 300 times.
Detailed description of the invention
Below by embodiment, the present invention is specifically described, it is necessary to it is pointed out here that be that following example are only used In being further described the present invention, it is impossible to be interpreted as limiting the scope of the invention, person skilled in art can The present invention made some nonessential improvement and adjustment according to the invention described above content.
Embodiment 1
The preparation method of methionine crystal formation I, as follows:
5-(β-first mercaptoethyl) hydantoin react with solution of potassium carbonate obtain containing in methionine potassium hydrolyzed solution Add the hydroxypropyl methyl cellulose of 200-300ppm, be passed through CO while stirring2、CO2The pressure that is passed through be 0.3Mpa, tie Partial crystallization goes out to obtain methionine crude product;
Above-mentioned methionine crude product is dissolved in sec-butyl alcohol solvent with the concentration of 25mg/mL-28mg/mL, is stirred continuously, adds Heat, to 70 DEG C~75 DEG C dissolvings, filters, and forms supersaturated solution;This solution is sealed and is placed on crystallisation by cooling in-6 DEG C of environment 2.5 hours, obtain white crystal.
Embodiment 2
By the methionine crystal obtained by embodiment 1, it is XRD and tests:
Radiation source is Cu target, and wavelength is 1.54060nm, and scanning angle is 10 °~70 °, and voltage is 30kV, and electric current is 20mA, scanning speed is 2.4 °/min.Its X-ray powder diffraction figure is as shown in Figure 1.
Described crystal type methionine angle of diffraction 2 θ 118.395 ± 0.2 °, 21.186 ± 0.2 °, 21.751 ± 0.2°、22.168±0.2°、23.301±0.2°、25.426±0.2°、32.879±0.2°、33.775±0.2°、37.054 ± 0.2 °, have diffraction maximum at 42.455 ± 0.2 °.
The crystal type methionine of the present invention, its powder X-ray diffraction pattern is with interplanar distance D, Bragg angle (2 θ), relative intensity Percentage ratio I (%) and intensity (I value) crystal formation are expressed, as follows:
The differential scanning calorimeter (DSC) of crystal type methionine of the present invention is as in figure 2 it is shown, its endothermic transition temperature is 282 ℃;Its thermogravimetric analysis figure (TG) is as in figure 2 it is shown, about 240 DEG C proceed by first reaction, and 282 DEG C carry out second reaction, Terminate to reaction when 380 DEG C.
Methionine crystal type granule scanning electron microscope (SEM) photograph under 300 times as it is shown on figure 3, its granule is relatively big, in near-spherical and Granularity concentrates on 110-130 micron, more uniform, excellent quality;After measured, its in water dissolubility at 5.0g/100g water.
Embodiment 3
The preparation method of methionine crystal formation I, employing following steps:
5-(β-first mercaptoethyl) hydantoin react with solution of potassium carbonate obtain containing in methionine potassium hydrolyzed solution Add the hydroxypropyl methyl cellulose of 50-100ppm, be passed through CO while stirring2、CO2The pressure that is passed through be 0.6Mpa, crystallize Precipitation obtains methionine crude product;
Above-mentioned methionine crude product is dissolved in sec-butyl alcohol solvent with the concentration of 10mg/mL-20mg/mL, is stirred continuously, adds Heat, to 60 DEG C~65 DEG C dissolvings, filters, and forms supersaturated solution;This solution is sealed and is placed on crystallisation by cooling 3 in-10 DEG C of environment Hour, obtain white crystal.
Identify by the method for embodiment 2, for methionine crystal formation I of the present invention, its in water dissolubility at 5.2g/100g water.
Embodiment 4
The preparation method of methionine crystal formation I, employing following steps:
5-(β-first mercaptoethyl) hydantoin react with solution of potassium carbonate obtain containing in methionine potassium hydrolyzed solution Add the hydroxypropyl methyl cellulose of 900-1000ppm, be passed through CO while stirring2、CO2The pressure that is passed through be 0.2Mpa, tie Partial crystallization goes out to obtain methionine crude product;
Above-mentioned methionine crude product is dissolved in sec-butyl alcohol solvent with the concentration of 40mg/mL-50mg/mL, is stirred continuously, adds Heat, to 95 DEG C~100 DEG C dissolvings, filters, and forms supersaturated solution;This solution is sealed and is placed on crystallisation by cooling 1 in-5 DEG C of environment Hour, obtain white crystal.
Identify by the method for embodiment 2, for methionine crystal formation I of the present invention, its in water dissolubility at 4.6g/100g water.
Embodiment 5
The preparation method of methionine crystal formation I, employing following steps:
5-(β-first mercaptoethyl) hydantoin react with solution of potassium carbonate obtain containing in methionine potassium hydrolyzed solution Add the hydroxypropyl methyl cellulose of 500-600ppm, be passed through CO while stirring2、CO2The pressure that is passed through be 0.4Mpa, tie Partial crystallization goes out to obtain methionine crude product;
Above-mentioned methionine crude product is dissolved in sec-butyl alcohol solvent with the concentration of 25mg/mL-35mg/mL, is stirred continuously, adds Heat, to 70 DEG C~80 DEG C dissolvings, filters, and forms supersaturated solution;The sealing of this solution is placed in-7 DEG C~-8 DEG C of environment and cools down Crystallize 2 hours, obtain white crystal.
Identify by the method for embodiment 2, for methionine crystal formation I of the present invention, its in water dissolubility at 4.8g/100g water.

Claims (7)

1. a methionine crystal formation I, it is characterised in that: described crystal formation I angle of diffraction 2 θ 21.751 ± 0.2 °, 22.168 ± 0.2 °, 21.186 ± 0.2 °, 25.426 ± 0.2 °, 18.395 ± 0.2 °, have diffraction maximum at 32.879 ± 0.2 °.
2. as claimed in claim 1 methionine crystal formation I, it is characterised in that: described crystal formation at angle of diffraction 2 θ 18.395 ± 0.2°、21.186±0.2°、21.751±0.2°、22.168±0.2°、23.301±0.2°、25.426±0.2°、32.879 ± 0.2 °, 33.775 ± 0.2 °, 37.054 ± 0.2 °, have diffraction maximum at 42.455 ± 0.2 °.
3. methionine crystal formation I as claimed in claim 1 or 2, it is characterised in that: the X-ray powder that it has as shown in Figure 1 spreads out Penetrate figure.
4. methionine crystal formation I as claimed in claim 1, it is characterised in that: it has followingValue and relative intensity hundred The expression of proportion by subtraction I (%) value-X-ray powder diffraction data,
5. the methionine crystal formation I as described in claim 1,2,3 or 4, it is characterised in that: it has followingValue is with relative The expression of intensity percent I (%) value-X-ray powder diffraction data:
6. methionine crystal formation I as claimed in claim 1 or 2, it is characterised in that: it has DSC/TG collection of illustrative plates as shown in Figure 2, its Melting point peak temperature is 282 DEG C.
7. the preparation method of methionine crystal formation I as described in any one of claim 1-6, it is characterised in that employing following steps:
(1), 5-(β-first mercaptoethyl) hydantoin react with solution of potassium carbonate obtain containing in methionine potassium hydrolyzed solution Add the hydroxypropyl methyl cellulose of 50-1000ppm, be passed through CO while stirring2、CO2The pressure that is passed through be that 0.2-0.6Mpa is left The right side, carries out crystallization and obtains methionine crude product;
(2), above-mentioned methionine crude product is dissolved in sec-butyl alcohol solvent with the concentration of 10mg/mL-50mg/mL, is stirred continuously, adds Heat, to 60 DEG C~100 DEG C dissolvings, filters, and forms supersaturated solution;The sealing of this solution is placed in-5 DEG C~-10 DEG C of environment cold But crystallization 1-3 hour, obtains white crystal.
CN201610391281.7A 2016-06-03 2016-06-03 A kind of methionine novel crystal forms I and preparation method thereof Active CN106083675B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017206703A1 (en) * 2016-06-03 2017-12-07 宁夏紫光天化蛋氨酸有限责任公司 Methionine new crystal form i and preparation method therefor

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JPS4324890B1 (en) * 1966-08-25 1968-10-28
CN1274717A (en) * 1999-05-21 2000-11-29 住友化学工业株式会社 Prepn. of methionine
CN1589259A (en) * 2001-11-29 2005-03-02 日本曹达株式会社 Process for production of methionine
CN1274717C (en) * 2002-11-06 2006-09-13 中国人民解放军军事医学科学院附属医院 Immune suppression fusion protein, its coded nucleic acid and application
CN1923807A (en) * 2005-08-29 2007-03-07 住友化学株式会社 Process for producing methionine
CN101003822A (en) * 2006-07-05 2007-07-25 中国科学院成都有机化学有限公司 Method for producing D amino acid by immobilizing acylation enzyme of penicillin
CN103641758A (en) * 2013-11-19 2014-03-19 重庆紫光化工股份有限公司 Cheap preparation method for high purity D,L-methionine
CN104203912A (en) * 2012-03-20 2014-12-10 赢创工业集团股份有限公司 Preparation method of methionine
CN104744326A (en) * 2015-02-12 2015-07-01 山东新和成氨基酸有限公司 Method for continuously preparing high-bulk density methionine crystals

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Publication number Priority date Publication date Assignee Title
JPS4324890B1 (en) * 1966-08-25 1968-10-28
CN1274717A (en) * 1999-05-21 2000-11-29 住友化学工业株式会社 Prepn. of methionine
CN1589259A (en) * 2001-11-29 2005-03-02 日本曹达株式会社 Process for production of methionine
CN1274717C (en) * 2002-11-06 2006-09-13 中国人民解放军军事医学科学院附属医院 Immune suppression fusion protein, its coded nucleic acid and application
CN1923807A (en) * 2005-08-29 2007-03-07 住友化学株式会社 Process for producing methionine
CN101003822A (en) * 2006-07-05 2007-07-25 中国科学院成都有机化学有限公司 Method for producing D amino acid by immobilizing acylation enzyme of penicillin
CN104203912A (en) * 2012-03-20 2014-12-10 赢创工业集团股份有限公司 Preparation method of methionine
CN103641758A (en) * 2013-11-19 2014-03-19 重庆紫光化工股份有限公司 Cheap preparation method for high purity D,L-methionine
CN104744326A (en) * 2015-02-12 2015-07-01 山东新和成氨基酸有限公司 Method for continuously preparing high-bulk density methionine crystals

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017206703A1 (en) * 2016-06-03 2017-12-07 宁夏紫光天化蛋氨酸有限责任公司 Methionine new crystal form i and preparation method therefor

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